JPH0145341B2 - - Google Patents
Info
- Publication number
- JPH0145341B2 JPH0145341B2 JP56145590A JP14559081A JPH0145341B2 JP H0145341 B2 JPH0145341 B2 JP H0145341B2 JP 56145590 A JP56145590 A JP 56145590A JP 14559081 A JP14559081 A JP 14559081A JP H0145341 B2 JPH0145341 B2 JP H0145341B2
- Authority
- JP
- Japan
- Prior art keywords
- silo
- fumigation
- methyl bromide
- surge tank
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Catching Or Destruction (AREA)
Description
【発明の詳細な説明】
本発明はくん蒸性能の悪い穀物その他に用いる
くん蒸装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fumigation apparatus for use with grains and other materials having poor fumigation performance.
従来のこの種装置としてくん蒸室と該室内に大
豆粕等を供給するコンベヤと該コンベヤの上方に
設けられたホストキシンの供給装置とからなり、
コンベヤによつて搬送中の大豆粕等の上に供給装
置から逐次ホストキシンを流下させ、これらの混
合物がくん蒸室内に所定量貯蔵された時点でその
供給を停止し該くん蒸室内で大豆粕等を数日間に
亘つてくん蒸するようにしたものが知られるが、
この従来装置によればくん蒸のためにホストキシ
ンを使用しており、このホストキシンは値段が高
く、大量のくん蒸を行うとすると費用が相当にか
かる欠点があつた。 A conventional device of this type consists of a fumigation chamber, a conveyor for supplying soybean meal, etc. into the chamber, and a hostoxin supply device installed above the conveyor.
Hostoxin is sequentially flowed down from the feeding device onto the soybean meal, etc. being transported by a conveyor, and when a predetermined amount of this mixture is stored in the fumigation chamber, the supply is stopped and the soybean meal, etc. is placed in the fumigation chamber. It is known that it was fumigated for several days,
This conventional device uses hostoxin for fumigation, and this hostoxin is expensive and has the disadvantage that fumigation in large quantities requires considerable cost.
そこでこのような値段の高いホストキシンの代
りに値段の安い臭化メチルを用いたサイロシステ
ムが提案された。即ちこのサイロシステムはサイ
ロの頂上部から真空ポンプで空気を抜いて該頂上
部を真空に近い状態に減圧しサイロ下部から加圧
空気を吹き込むことによつて大豆粕等粉粒体の貯
蔵物を流動化させる方式であるが、この方式によ
ればサイロの頂部は真空に近い反面該サイロの下
部は高圧となり、同一サイロの上下で相当の圧力
差があり、この大きな圧力差により該サイロの壁
面にかなり内部応力が生じ、かくてこの内部応力
に打克つべく該壁面の肉厚を大にしなければなら
ず、サイロの設備費が大となる欠点がある。 Therefore, a silo system using cheap methyl bromide instead of expensive hostoxin was proposed. In other words, this silo system removes stored materials such as soybean meal and other powder by removing air from the top of the silo using a vacuum pump, reducing the pressure at the top to a near-vacuum state, and then blowing pressurized air from the bottom of the silo. This is a fluidization method, but with this method, the top of the silo is close to vacuum, but the bottom of the silo is under high pressure, and there is a considerable pressure difference between the top and bottom of the same silo, and this large pressure difference causes the walls of the silo to Considerable internal stress is generated in the silo, and in order to overcome this internal stress, the wall thickness must be increased, which has the disadvantage of increasing the equipment cost of the silo.
本発明はこれらの欠点を解消したくん蒸装置を
提供することを目的とするもので、その要旨は穀
類等を貯蔵したサイロの頂上部から下部に循環管
路を接続し、該循環管路に、前記サイロの下部内
に臭化メチルガスをパルス状に加圧流入する加圧
流入装置と、前記サイロの頂上部からの排出ガス
を収容するサージタンクを介在し、該サイロ内を
大気圧以上にしてくん蒸することにある。 The purpose of the present invention is to provide a fumigation device that eliminates these drawbacks.The gist of the present invention is to connect a circulation pipe from the top to the bottom of a silo storing grains, etc., and to the circulation pipe, A pressurized inflow device for pressurized methyl bromide gas to flow into the lower part of the silo in a pulsed manner and a surge tank for accommodating exhaust gas from the top of the silo are interposed, and the inside of the silo is raised to above atmospheric pressure. It involves fumigation.
以下本発明の1実施例を図面に従つて説明す
る。 An embodiment of the present invention will be described below with reference to the drawings.
1はサイロを示し、該サイロ1の頂部1aに穀
類を入れるための流入口1b及び下部1cに穀類
を排出する排出口1dを具備し、これら流入口1
b及び排出口1dには内部を密閉する蓋或いはゲ
ートを有している。2は加圧流入装置を示し、該
装置2は前記サイロ1の下部1cに管路3aを介
して連通するレシーバータンク2aと該レシーバ
ータンク2aに管路3bを介して連通するコンプ
レツサー2bを該レシーバータク2aと臭化メチ
ルボンベ4との間を連通する管路3cに介在した
気化器2cと前記管路3aに介在した開閉制御弁
2dとからなり、臭化メチルボンベ4内の液化臭
化メチルを気化器2cにおいて気化したレシーバ
ータンク2aに供給すると共にコンプレツサー2
bからの加圧空気も該レシーバータンク2aに供
給し、該タンク2a内において希釈した加圧臭化
メチルガスにし該ガスを開閉制御弁2dの断続的
開閉によりサイロ1の下部1cに断続的即ちパル
ス状に加圧流入するようにした。 Reference numeral 1 designates a silo, and the top portion 1a of the silo 1 is equipped with an inlet 1b for introducing grains, and the lower portion 1c is provided with an outlet 1d for discharging grains.
b and the discharge port 1d have a lid or a gate to seal the inside. 2 denotes a pressurized inflow device, which includes a receiver tank 2a communicating with the lower part 1c of the silo 1 via a pipe 3a, and a compressor 2b communicating with the receiver tank 2a via a pipe 3b. It consists of a vaporizer 2c interposed in a pipe line 3c communicating between the tank 2a and the methyl bromide cylinder 4, and an on-off control valve 2d interposed in the pipe line 3a. is supplied to the receiver tank 2a where it is vaporized in the vaporizer 2c, and the compressor 2
The pressurized air from b is also supplied to the receiver tank 2a, and the gas is converted into diluted pressurized methyl bromide gas in the tank 2a, and the gas is intermittently or pulsed to the lower part 1c of the silo 1 by the intermittent opening and closing of the on-off control valve 2d. It was made to flow under pressure.
5は前記サイロ1の頂部1aに管路3dを介し
て連通したサージタンクを示し、該タンク5の容
積はサイロ1の容積並に加圧流入される臭化メチ
ルガスの量に応じて定められる。 Reference numeral 5 denotes a surge tank connected to the top 1a of the silo 1 via a pipe 3d, and the volume of the tank 5 is determined according to the volume of the silo 1 and the amount of methyl bromide gas fed under pressure.
6はブロワ、3eは前記サージタンク5とブロ
ワ6の吸入側を連通する管路、3fは前記管路3
bの中間より分岐して前記ブロワ6の吐出側に連
通する管路、3gは前記管路3eのサージタンク
5の近傍から分岐して先端が大気に開放する管
路、3hは該管路3eのブロワの近傍から分岐し
て先端が大気に開放する管路、3iは前記管路3
eから分岐してコンプレツサー2bに連る管路を
示し、前記管路3a,3d,3e,3f及び3b
或いは管路3a,3d,3e,3i及び3bによ
り循環管路を形成した。 6 is a blower, 3e is a pipe connecting the surge tank 5 and the suction side of the blower 6, and 3f is the pipe 3
A pipe line 3g branches from the middle of the pipe line 3e and communicates with the discharge side of the blower 6, a pipe line 3g branches from the vicinity of the surge tank 5 of the pipe line 3e and its tip is open to the atmosphere, and a pipe line 3h indicates the pipe line 3e. 3i is the pipe line 3 which branches from near the blower and whose tip is open to the atmosphere.
shows a pipe branching from e and leading to the compressor 2b, and the pipes 3a, 3d, 3e, 3f and 3b
Alternatively, a circulation pipe was formed by pipes 3a, 3d, 3e, 3i, and 3b.
尚、7a,7b,7c,7d,7e,7f,7
g,7h,7i,7j及び7kは図示の如く管路
にそれぞれ介入した開閉弁を示す。 In addition, 7a, 7b, 7c, 7d, 7e, 7f, 7
g, 7h, 7i, 7j and 7k indicate on-off valves respectively inserted in the pipelines as shown.
次に上記実施例装置の作動を説明する。 Next, the operation of the above embodiment device will be explained.
サイロ1の排出口1dを密閉すると共に流入口
1bを開放し、該流入口1bから例えば大豆粕を
サイロ1内に所定量貯蔵して前記流入口1bを密
閉する。然る後開閉制御弁2dを所定回数断続的
に開閉しレシーバータンク2aから希釈臭化メチ
ルガスをサイロ1の下部にパルス状に加圧流入す
る。このパルス状の加圧流入にすれば大豆粕は流
動化して大豆粕はその大部分が均一に臭化メチル
ガスとの接触状態になる。そして余つたガスはサ
ージタンク5内に逐次流入収容されていく。尚こ
の臭化メチルガスのサイロ1内への充満の程度は
該サイロ1の上部、中間部及び下部に装備した濃
度計によりチエツクし未だ均一に充満されていな
いときには開閉弁7d,7f,7h,7jを開け
ると共にブロワ6を駆動してサージタンク5内に
集められた余つた臭化メチルガスを循環させて再
使用してサイロ1内において均一な充満を達成す
る。従つて臭化メチルガスが有効に利用されて経
済的である。又、この充満を高圧の圧送により早
期に達成したい場合は、開閉弁7hを閉じると共
に開閉弁7k及び7iを開放してコンプレツサー
2bを駆動し管路3iを用いて行う。ここでサー
ジタンク5は、サイロ1から排出の臭化メチルガ
スを集めて収容する機能と、臭化メチルガスを循
環して運転するとき、サイロ1の下部1cにパル
ス状に加圧流入した該ガスをサージタンク5にお
いてパルス状の脈動流を鎮静化させブロワ6の安
定運転を達成する機能を有する。このようにサー
ジタンク5内は、予め大気圧の状態でその後前述
した如くパルス状に加圧流入した臭化メチルガス
を、サイロ1内の大豆粕間の通過後管路3dを介
して集める式であるので、該サイロ1の頂上部1
aは大気圧以上となり下部1aの圧力との差が従
来のサイロシステムと比べてかなり小さくなりか
くてサイロ1の壁面に作用する内部応力が小とな
り該壁面の肉厚は薄くともよい。 The discharge port 1d of the silo 1 is sealed, and the inflow port 1b is opened, and a predetermined amount of soybean meal, for example, is stored in the silo 1 from the inflow port 1b, and the inflow port 1b is sealed. Thereafter, the opening/closing control valve 2d is intermittently opened and closed a predetermined number of times, and the diluted methyl bromide gas flows into the lower part of the silo 1 under pressure in a pulsed manner from the receiver tank 2a. By applying this pulsed pressurized inflow, the soybean meal is fluidized and most of the soybean meal is uniformly brought into contact with the methyl bromide gas. Then, the remaining gas is successively introduced into the surge tank 5 and stored therein. The degree to which the silo 1 is filled with methyl bromide gas is checked using concentration meters installed at the top, middle, and bottom of the silo 1, and if the silo 1 is not evenly filled, the on-off valves 7d, 7f, 7h, and 7j are activated. When the silo 1 is opened, the blower 6 is driven to circulate and reuse the surplus methyl bromide gas collected in the surge tank 5 to achieve uniform filling in the silo 1. Therefore, methyl bromide gas is effectively utilized and is economical. If it is desired to quickly achieve this filling by high-pressure pumping, the on-off valve 7h is closed, the on-off valves 7k and 7i are opened, the compressor 2b is driven, and the conduit 3i is used. Here, the surge tank 5 has the function of collecting and storing the methyl bromide gas discharged from the silo 1, and when operating by circulating the methyl bromide gas, the surge tank 5 has the function of collecting and storing the methyl bromide gas discharged from the silo 1. It has a function of suppressing the pulsating flow in the surge tank 5 and achieving stable operation of the blower 6. In this way, the inside of the surge tank 5 has a system in which the methyl bromide gas, which has been previously brought into the atmosphere at atmospheric pressure and then flows under pressure in a pulsed manner as described above, is collected via the pipe line 3d after passing between the soybean meal in the silo 1. Therefore, the top part 1 of the silo 1
a is higher than the atmospheric pressure, and the difference from the pressure in the lower part 1a is considerably smaller than in conventional silo systems, so the internal stress acting on the wall of the silo 1 is small, and the wall thickness of the wall may be thin.
サイロ1内の臭化メチルガス濃度が所定の均一
化が行われた後該ガスの加圧流入を停止してサイ
ロ1内で大豆粕は約48時間かけてくん蒸する。そ
してくん蒸の終了後サイロ1の排出口1dを開放
し、開閉弁7bを閉じて開閉制御弁2dを断続的
開聞させて空気をレシーバータンク2aからサイ
ロ1の下部1c内にパルス状に加圧流入しくん蒸
後の大豆粕をブリツジを生じさせることなく円滑
にサイロ1から排出させる。 After the concentration of methyl bromide gas in the silo 1 is equalized to a predetermined level, the pressurized flow of the gas is stopped, and the soybean meal is fumigated in the silo 1 for about 48 hours. After the fumigation is completed, the discharge port 1d of the silo 1 is opened, the on-off valve 7b is closed, and the on-off control valve 2d is opened intermittently to allow air to flow under pressure from the receiver tank 2a into the lower part 1c of the silo 1 in a pulsed manner. To smoothly discharge soybean meal after fumigation from a silo 1 without causing bridging.
尚サイロ1内のクリーニングは該サイロ1内を
空にして前述の如く該サイロ1の下部1cに空気
をパルス状に加圧流入し、頂上部1aから空気を
サージタンク5に集めるようにすればよい。 The inside of the silo 1 can be cleaned by emptying the inside of the silo 1, pressurizing air into the lower part 1c of the silo 1 in a pulsed manner as described above, and collecting the air from the top part 1a into the surge tank 5. good.
このように本発明によれば臭化メチルガスによ
るくん蒸であるので安価にくん蒸ができると共
に、加圧入装置によりサイロ内に臭化メチルガス
をパルス状に加圧流入し、該サイロ内を大気圧以
上にしてくん蒸するようにしたので、該サイロ内
は該メチルガスにより大気圧より大となつて該サ
イロの周壁に引張応力が作用し、かくて該サイロ
は一般的に鋼材からなり該鋼材は引張強度でが大
であるため該サイロの周壁の肉厚を薄くすること
が可能となり設備費を小とすることができ、又前
記サージタンクにより前記サイロの下部にパルス
状に加圧流入した臭化メチルガスのパルス状の脈
動流を鎮静化し、かくて加圧流入装置において該
ガスのパルス状の脈動流に影響されずに正確なパ
ルス状の臭化メチルガスの加圧流入をサイロの下
部に確実に行え、更にくん蒸性能の悪い穀物につ
いて完全なるくん蒸を達成し得る効果を有する。 As described above, according to the present invention, since fumigation is performed using methyl bromide gas, it is possible to perform the fumigation at a low cost, and methyl bromide gas is injected into the silo under pressure in a pulsed manner using a pressurization device to raise the inside of the silo to atmospheric pressure or higher. Because of the fumigation, the pressure inside the silo becomes higher than atmospheric pressure due to the methyl gas, and tensile stress acts on the peripheral wall of the silo.The silo is generally made of steel, and the steel has a high tensile strength. Since the silo is large, it is possible to reduce the wall thickness of the peripheral wall of the silo, thereby reducing equipment costs, and the methyl bromide gas that flows under pressure into the lower part of the silo in a pulsed manner by the surge tank can be reduced. The pulsating pulsating flow is suppressed, and thus the pressurized inflow device is able to ensure accurate pulsating pressurized inflow of methyl bromide gas into the lower part of the silo without being affected by the pulsating pulsating flow of the gas, Furthermore, it has the effect of achieving complete fumigation for grains with poor fumigation performance.
図面は本発明装置の1例のフローシート図であ
る。
1……サイロ、1a……頂上部、1c……下
部、2……加圧流入装置、5……サージタンク。
The drawing is a flow sheet diagram of an example of the apparatus of the present invention. 1... Silo, 1a... Top part, 1c... Lower part, 2... Pressurized inflow device, 5... Surge tank.
Claims (1)
循環管路を接続し、該循環管路に、前記サイロの
下部内に臭化メチルガスをパルス状に加圧流入す
る加圧流入装置と、前記サイロの頂上部からの排
出ガスを収容するサージタンクを介在し、該サイ
ロ内を大気圧以上にしてくん蒸することを特徴と
するくん蒸装置。1. A pressurized inflow device that connects a circulation pipe from the top to the bottom of a silo in which grains, etc. are stored, and flows methyl bromide gas under pressure into the lower part of the silo into the circulation pipe; A fumigation device characterized by interposing a surge tank that accommodates exhaust gas from the top of a silo, and performing fumigation by raising the inside of the silo to atmospheric pressure or higher.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14559081A JPS5847423A (en) | 1981-09-17 | 1981-09-17 | Smoking apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14559081A JPS5847423A (en) | 1981-09-17 | 1981-09-17 | Smoking apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5847423A JPS5847423A (en) | 1983-03-19 |
| JPH0145341B2 true JPH0145341B2 (en) | 1989-10-03 |
Family
ID=15388598
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14559081A Granted JPS5847423A (en) | 1981-09-17 | 1981-09-17 | Smoking apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5847423A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5398274A (en) * | 1977-02-09 | 1978-08-28 | Tsuneyuki Iwata | Method for fumigation silo cereals and preventing bridging |
-
1981
- 1981-09-17 JP JP14559081A patent/JPS5847423A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5847423A (en) | 1983-03-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS58155269A (en) | Method and device for supplying engine with liquid fuel by gas pressure | |
| US8156857B2 (en) | Equipment for the rehydration of yeasts, in particular for oenology | |
| US3345992A (en) | Method for conditioning tobacco | |
| CN110063324B (en) | A storage insecticidal system | |
| JPH0145341B2 (en) | ||
| JP2008272703A (en) | Method for cleaning inside of piping of pneumatic transportation apparatus and pneumatic transportation apparatus | |
| JPH10263379A (en) | Automatic dilution device | |
| CN213769942U (en) | Raw materials storage tank device of unloading | |
| GB940555A (en) | Method of and apparatus for aerating liquids | |
| US3262458A (en) | Method and apparatus for conditioning tobacco | |
| JPH01181624A (en) | Pneumatic transport method and device for resin material | |
| JPS641144B2 (en) | ||
| JPS6127092B2 (en) | ||
| SU475328A1 (en) | Chamber feeder of pneumatic injection system for transporting bulk materials | |
| RU2026249C1 (en) | Continuous-action chamber pump for pneumatic transportation of loose material | |
| CN213463616U (en) | Pressure device and pesticide preparation equipment | |
| RU2081599C1 (en) | Grain preservation apparatus | |
| CN208300823U (en) | A kind of phosphine circulation device reacted and conveying speed is controllable | |
| CN207313140U (en) | A kind of phosphatization apparatus for forming hydrogen | |
| JPS63310419A (en) | Powder and granule high concentration pneumatic transport equipment | |
| JP2550905Y2 (en) | Fumigation equipment | |
| JPS609456B2 (en) | How to vent gas in a gas sterilizer | |
| JPH0361822B2 (en) | ||
| JPH0468004B2 (en) | ||
| RU49682U1 (en) | DEVICE FOR SMOKING FOOD PRODUCTS (ATOMIZER) |